Influence of pH, temperature and initial yeast: bacteria ratio on the stimulation of Lactobacillus hilgardii by Saccharomyces florentinus isolated from sugary kefir grains

The effects of pH, temperature and initial yeast: bacteria ratio on Lactobacillus hilgardii and Saccharomyces florentinus cultivated either in pure or mixed culture were studied. Quadratic polynomial as a function of factors was proposed to express the lactic acid production at different sampling times, and the percentage increase in lactic acid production by Lact. hilgardii in mixed culture compared with pure culture. Temperature was the factor which had the main influence on lactic acid production in mixed culture, whereas stimulation of bacteria depended greatly on pH value. In the range 0·1-20%, the initial yeast: bacteria ratio had no effect on these responses, but presence of the yeast was absolutely necessary to obtain high production of lactic acid. Optimum culture conditions were determined to maximize these characteristics.     

Detection of interactions between yeasts and lactic acid bacteria isolated from sugary kefir grains

Different techniques were tested for studying the synergism between the micro-organisms of sugary kefir grains. Agar cultures in Petri dishes did not give reproducible results. In sequential cultures, i.e. growing one organism, sterile filtering and then inoculating the other, 10 of 18 selected lactic acid bacteria/yeast pairs revealed stimulation of bacterial growth in a poor glucose medium. In mixed culture, Saccharomyces florentinus supported better survival of Lactobacillus hilgardii and a significant increase in lactic acid production; at the same time, the growth and alcoholic fermentation of S. florentinus were drastically reduced. The inter-relationships between these two strains were the same when immobilized in calcium alginate beads, even though total metabolite production was always lower than with free cells. The stimulation of Lact. hilgardii by Candida lambica in sequential culture was not confirmed in mixed culture, where the two organisms grew as in pure culture, and bacterial growth and lactic acid production were inhibited in the immobilized system.     

Decarboxylation of substituted cinnamic acids by lactic acid bacteria isolated during malt whisky fermentation

Seven strains of Lactobacillus isolated from malt whisky fermentations and representing Lactobacillus brevis, L. crispatus, L. fermentum, L. hilgardii, L. paracasei, L. pentosus, and L. plantarum contained genes for hydroxycinnamic acid (p-coumaric acid) decarboxylase. With the exception of L. hilgardii, these bacteria decarboxylated p-coumaric acid and/or ferulic acid, with the production of 4-vinylphenol and/or 4-vinylguaiacol, respectively, although the relative activities on the two substrates varied between strains. The addition of p-coumaric acid or ferulic acid to cultures of L. pentosus in MRS broth induced hydroxycinnamic acid decarboxylase mRNA within 5 min, and the gene was also induced by the indigenous components of malt wort. In a simulated distillery fermentation, a mixed culture of L. crispatus and L. pentosus in the presence of Saccharomyces cerevisiae decarboxylated added p-coumaric acid more rapidly than the yeast alone but had little activity on added ferulic acid. Moreover, we were able to demonstrate the induction of hydroxycinnamic acid decarboxylase mRNA under these conditions. However, in fermentations with no additional hydroxycinnamic acid, the bacteria lowered the final concentration of 4-vinylphenol in the fermented wort compared to the level seen in a pure-yeast fermentation. It seems likely that the combined activities of bacteria and yeast decarboxylate p-coumaric acid and then reduce 4-vinylphenol to 4-ethylphenol more effectively than either microorganism alone in pure cultures. Although we have shown that lactobacilli participate in the metabolism of phenolic compounds during malt whisky fermentations, the net result is a reduction in the concentrations of 4-vinylphenol and 4-vinylguaiacol prior to distillation.     

氮源对灵芝菌丝体液态深层发酵合成灵芝三萜的影响

以沪农灵芝1号为供试菌株,葡萄糖作为碳源,用硫酸铵、氯化铵、鱼粉蛋白胨、胰蛋白胨和酵母粉作为氮源,研究不同种类氮源对灵芝菌丝体液态深层发酵过程的影响。首先,确定了N-10酵母自溶粉作为发酵的氮源,降低了发酵的复杂性和不确定性;其次,考察N-10酵母自溶粉不同浓度对灵芝菌丝体发酵合成灵芝三萜过程中菌丝体的生物量、葡萄糖消耗、灵芝三萜产量等方面的影响,确定了N-10酵母自溶粉的适宜添加浓度。在此基础上,采用响应面中心组合设计,对4因素最佳水平范围进行研究,结果表明,葡萄糖、N-10酵母自溶粉、磷酸二氢钾和七水硫酸镁的含量分别为31.06g/L、2.76g/L、1.77g/L和1.99g/L时,灵芝三萜的理论产量为21.166g/kg干菌丝体,实际发酵产量提高到21.153g/kg干菌丝体。与原工艺相比,新工艺的灵芝三萜产量提高了6.22%。     

Screening of Ganoderma strains with high polysaccharides and ganoderic acid contents and optimization of the fermentation medium by statistical methods

Polysaccharides and ganoderic acids (GAs) are the major bioactive constituents of Ganoderma species. However, the commercialization of their production was limited by low yield in the submerged culture of Ganoderma despite improvement made in recent years. In this work, twelve Ganoderma strains were screened to efficiently produce polysaccharides and GAs, and Ganoderma lucidum 5.26 (GL 5.26) that had been never reported in fermentation process was found to be most efficient among the tested stains. Then, the fermentation medium was optimized for GL 5.26 by statistical method. Firstly, glucose and yeast extract were found to be the optimum carbon source and nitrogen source according to the single-factor tests. Ferric sulfate was found to have significant effect on GL 5.26 biomass production according to the results of Plackett–Burman design. The concentrations of glucose, yeast extract and ferric sulfate were further optimized by response surface methodology. The optimum medium composition was 55 g/L of glucose, 14 g/L of yeast extract, 0.3 g/L of ferric acid, with other medium components unchanged. The optimized medium was testified in the 10-L bioreactor, and the production of biomass, IPS, total GAs and GA-T enhanced by 85, 27, 49 and 93 %, respectively, compared to the initial medium. The fermentation process was scaled up to 300-L bioreactor; it showed good IPS (3.6 g/L) and GAs (670 mg/L) production. The biomass was 23.9 g/L in 300-L bioreactor, which was the highest biomass production in pilot scale. According to this study, the strain GL 5.26 showed good fermentation property by optimizing the medium. It might be a candidate industrial strain by further process optimization and scale-up study.     

The capacity of orotic acid production in pyrimidinedeficient mutants ofBrevibacterium ammoniagenes

Eight uracil-dependent mutants ofBrevibacterium ammoniagenes CCEB 364 and three mutants ofCorynebacterium sp. 9366 were checked for the production of precursors of nucleic acids. Four of the strains liberated into the medium a substantial amount of orotic acid. The production of orotic acid by a mutant ofBrevibacterium ammoniagenes (1043) was examined on mineral media containing varying amounts of glucose in the presence of uracil. The optimum concentration of glucose for the production of orotic acid was found to be 5–8%. On media to which natural substrates were added the orotic acid production increased substantially. The maximum production (6.5 g orotic acid/liter) was reached in a medium containing 0.5% yeast extract and 5% glucose; addition of uracil to this medium had no effect on the production. The maximum rate of production occurred between 24 and 72 h of fermentation. After this period the concentration of orotic acid in the medium decreases.     

被孢霉γ-亚麻酸高产菌株选育

利用紫外线复合氯化锂诱变高山被孢霉SM96,筛选出一株高产γ-亚麻酸的菌株TM11,产量比出发菌株(25mg/L)提高了近3倍。对影响其多不饱和脂肪酸产生的因子Mg2+,VB6,营养盐溶液,磷源,碳源,氮源酵母膏进行了正交试验,选出TM11最佳的培养基配方:MgSO4·7H2O1.0g,VB6150mg/L,酵母膏6g/L,葡萄糖100g/L,营养盐溶液1mL/L,K2HPO42g/L。在上述最佳培养基中TM11的生物量达18.0213g/L,总脂达10.8128g/L,GLA量达668mg/L。     

PANTOTHENIC ACID AND THE UTILIZATION OF GLUCOSE BY LIVING AND CELL-FREE SYSTEMS

1. Added pantothenic acid was found to have no appreciable effect on the fermentation of glucose when used in conjunction with preparations of dialyzed yeast maceration juice or acetone-precipitated yeast maceration juice. 2. Addition of pantothenic acid failed to affect the rate of phosphorylation of glucose or the rate of decarboxylation of pyruvic acid by yeast maceration juice. 3. Pantothenic acid showed no effect on the rate of glycolysis by homogenized deficient chick tissues. 4. The accelerating effect of pantothenic acid on fermentation by deficient yeast cells was found to be accompanied by a "binding" of pantothenic acid by the yeast cells.     

Factors affecting membrane fouling in filtration of Saccharomyces cerevisiae in an internal ceramic filter bioreactor

Filtration of ethanol fermentation medium and broth by using symmetric and asymmetric ceramic membranes has been studied in an internal filter bioreactor. Factors studied included membrane structure and pore size, medium sterilization, and concentrations of glucose, yeast extract in the medium, yeast cell and protein in broth. The aim was to determine the main factors responsible for the decline in filtration performance during ethanol fermentation by Saccharomyces cerevisiae. Flux index (Fi) of a new concept has been developed to evaluate the degree of flux decline during the membrane fouling process. Fi was defined as the ratio of the membrane flux at certain filtration time (t?=?t) to the initial (t?=??0) flux of pure water, not the initial (t?=?+0) flux of the test fluid. Flux with sterilized medium was approximately two-fold higher than that with unsterilized medium although the reason could not be explained clearly. Glucose, interaction between glucose and yeast extract, yeast cells, and proteins in fermentation broth were found to play an important part in membrane fouling. Fi of the symmetric membrane decreased to a less extent than that of the asymmetric membrane with increasing glucose concentration. But, the result with various yeast cell concentrations turned out to be contrary. Fouling was more serious for asymmetric membrane during the filtration of fermentation supernatant. This was thought to be due to different fouling mechanisms for the two types of membrane.     

响应面分析法优化耐高温蛋白酶发酵培养基

采用响应面分析方法对产耐高温蛋白酶的苏云金芽孢杆菌(Bacillus thuringien- sis)FZ62发酵培养基进行优化．首先,进行发酵培养基碳源、氮源及初始pH值的单因素筛选,优化结果表明最适氮源为酵母粉、碳源是葡萄糖,初始pH值范围6-8．在此基础经响应面法优化,发酵培养基最佳组合为:酵母粉2．04%,葡萄糖为0．10%,初始pH7．07．经以上优化后发酵水平比初始设计提高了3．22倍．     

Ethanol fermentation of crude acid hydrolyzate of cellulose using high-level yeast inocula

High-level yeast inocula was investigated as a means of overcoming the toxicity problem in ethanol fermentation of acid hydrolyzate of wood cellulose. When the inoculum level exceeded 10(8) initial cells/mL, 50% of the yeast cells survived the initial cell death period during which furfural and HMF were depleted. The fermentation thus proceeded to completion by virtue of cell regrowth. The specific ethanol productivity in batch fermentation on the basis of viable cells was comparable to that of pure glucose fermentation. Continuous fermentation with cell recycle was superior to batch fermentation in that there was no overall cell decline and the ethanol yield was substantially higher. The maximum ethanol productivity in continuous fermentation was 4.9 g/L h and it occurred at a dilution rate of 0.24 hr(-1).     

Extractive lactic acid fermentation in poly (ethyleneimine)-based aqueous two-phase system

The potential of an aqueous two-phase system composed of a polycation, poly(ethyleneimine) (PEI), and an uncharged polymer, (hydroxyethyl) cellulose (HEC), for extractive lactic acid fermentation was tested. Batch fermentation with 20 g/L glucose in two-phase medium using Lactococcus lactis without external pH control resulted in 3-4 times higher amount of lactate and biomass produced as compared to that in a conventional one-phase medium. Lactic acid was preferentially partitioned to the PEI-rich bottom phase. However, the cells which favored the HEC-rich top phase in a fresh two-phase medium were partitioned to a significant extent to the bottom phase after fermentation. Addition of phosphate buffer or pH adjustment to 6.5 after fermentation caused fewer cells to move to the bottom phase. With external pH control, fermentation in normal and two-phase medium showed no marked differences in glucose consumption and lactic acid yield, except that about 1.3 times higher cell density was obtained in the two-phase broth, especially at initial glucose concentrations of 50-100 g/L. Use of higher concentration of phosphate during batch fermentation in the two-phase medium with 50 g/L sugar provided a 15% higher yield of lactic acid, but the growth rate of cells was nearly half of the normal, thus affecting the productivity. Continuous fermentation with twice the normal phosphate concentration resulted in higher cell density, product yield, and productivity in two-phase medium than in monophasic medium. (c) 1996 John Wiley & Sons, Inc.     

休哈塔假丝酵母乙醇发酵性能的研究

木糖的高效发酵是制约纤维素燃料乙醇生产的技术瓶颈之一,高性能发酵菌种的开发是本领域研究的重点。以木糖发酵的典型菌株休哈塔假丝酵母为材料,研究氮源配比、葡萄糖和木糖初始浓度、葡萄糖添加及典型抑制物等因素对其木糖利用和乙醇发酵性能的影响规律。结果表明,硫酸铵更适宜于木糖和葡萄糖发酵产乙醇。在摇瓶振荡发酵条件下,该酵母可发酵164.0 g/L葡萄糖生成61.9 g/L乙醇,糖利用率和乙醇得率分别为99.8%和74.0%;受酵母细胞膜上转运体系的限制,对木糖的最高发酵浓度为120.0 g/L,可生成45.7 g/L乙醇,糖利用率和乙醇得率分别达到94.8%和87.0%。休哈塔假丝酵母发酵木糖的主要产物为乙醇,仅生成微量的木糖醇;添加葡萄糖可促进木糖的利用;休哈塔假丝酵母在葡萄糖发酵时的乙酸和甲酸的耐受浓度分别为8.32和2.55 g/L,木糖发酵时的乙酸和甲酸的耐受浓度分别为6.28和1.15 g/L。     

Statistical optimization of the medium composition by response surface methodology to enhance schizophyllan production by Schizophyllum commune

The response surface methodology (RSM) involving central composite design (CCD) was employed to optimize the fermentation medium for the cell growth and schizophllan production by Schizophyllum commune CGMCC 5.113 in submerged culture at pH 6.5 and 26 degrees C. The four variables involved in this study were glucose, yeast extract, ammonium nitrate, and magnesium sulfate. The statistical analysis of the results showed that, in the range studied, glucose and yeast extract had a highly significant effect on schizophyllan production. The optimal medium for schizophyllan production calculated from the regression model of RSM was as follows: glucose, 18 g/l; yeast extract, 0.5 g/l; NH4NO3, 0.48 g/l; and MgSO4, 0.05 g/l, with a predicted maximum schizophyllan production of 11.74 g/l. These predicted values were experimentally validated. The excellent correlation between predicted and measured values justifies the validity of the response model. The results of bioreactor fermentation also show that the optimized medium enhanced schizophyllan production (12.80 g/l) by S. commune in a 5-1 fermenter.     

Enhanced Biosynthesis of Sulfide Oxidase by Arthrobacter Species Using Response Surface Methodology

Response surface methodology was used to develop a fermentation medium for the enhanced biosynthesis of a novel sulfide oxidase by Arthrobacter species strain FR‐3. The interactive effect of the medium components – such as glucose as the carbon source, and tryptone and yeast extract as the nitrogen source – was evaluated by a 2³‐factorial central composite statistical design. Glucose and yeast extract were found to be the more influential medium constituents compared to tryptone since they had lower coefficients of linear effect, P‐values (< 0.02). The optimal fermentation medium components for the enhanced production of sulfide oxidase were recorded as glucose (8.98 g/L), tryptone (10.62 g/L) and yeast extract (7.3 g/L). Optimization of the medium constituents increased the experimental enzyme yield by 54 % compared to the unoptimized medium. This is the first report on the overproduction of sulfide oxidase by using response surface methodology.     

L-乳酸调控乳酸产生菌产物光学纯度的分析

发酵初期在米根霉菌发酵培养基中添加L-乳酸可以调控发酵产物乳酸的光学纯度。随着L-乳酸添加量的增加,所产L-乳酸的光学纯度随之增加,当L-乳酸的添加量≥1.5g/L时,D-乳酸不再产生。同时,L-乳酸的产量、生物量、糖转化率也随之降低。该调控方法对乳酸菌调控产L-乳酸光学纯度影响不大,对大肠杆菌发酵调控产D-乳酸光学纯度没有效果。     

Caffeic acid production by simultaneous saccharification and fermentation of kraft pulp using recombinant Escherichia coli

Caffeic acid (3,4-dihydroxycinnamic acid) serves as a building block for thermoplastics and a precursor for biologically active compounds and was recently produced from glucose by microbial fermentation. To produce caffeic acid from inedible cellulose, separate hydrolysis and fermentation (SHF) and simultaneous saccharification and fermentation (SSF) reactions were compared using kraft pulp as lignocellulosic feedstock. Here, a tyrosine-overproducing Escherichia coli strain was metabolically engineered to produce caffeic acid from glucose by introducing the genes encoding a 4-hydroxyphenyllactate 3-hydroxylase (hpaBC) from Pseudomonas aeruginosa and tyrosine ammonia lyase (fevV) from Streptomyces sp. WK-5344. Using the resulting recombinant strain, the maximum yield of caffeic acid in SSF (233 mg/L) far exceeded that by SHF (37.9 mg/L). In the SSF with low cellulase loads (≤2.5 filter paper unit/g glucan), caffeic acid production was markedly increased, while almost no glucose accumulation was detected, indicating that the E. coli cells experienced glucose limitation in this culture condition. Caffeic acid yield was also negatively correlated with the glucose concentration in the fermentation medium. In SHF, the formation of by-product acetate and the accumulation of potential fermentation inhibitors increased significantly with kraft pulp hydrolysate than filter paper hydrolysate. The combination of these inhibitors had synergistic effects on caffeic acid fermentation at low concentrations. With lower loads of cellulase in SSF, less potential fermentation inhibitors (furfural, 5-hydroxymethyfurfural, and 4-hydroxylbenzoic acid) accumulated in the medium. These observations suggest that glucose limitation in SSF is crucial for improving caffeic acid yield, owing to reduced by-product formation and fermentation inhibitor accumulation.

     

Influence of Glucose and Saturated Free-Fatty Acid Mixtures on Citric Acid and Lipid Production by Yarrowia lipolytica

In the present report, the effect of glucose and stearin (substrate composed by saturated free-fatty acids) on the production of biomass, reserve lipid, and citric acid by Yarrowia lipolytica ACA-DC 50109 was investigated in nitrogen-limited cultures. Numerical models that were used in order to quantify the kinetic behavior of the above Yarrowia lipolytica strain showed successful simulation, while the optimized parameter values were similar to those experimentally measured and the predictive ability of the models was satisfactory. In nitrogen-limited cultures in which glucose was used as the sole substrate, satisfactory growth and no glucose inhibition occurred, although in some cases the initial concentration of glucose was significantly high (150 g/l). Citric acid production was observed in all trials, which was in some cases notable (final concentration 42.9 g/l, yield 0.56 g per g of sugar consumed). The concentration of unsaturated cellular fatty acids was slightly lower when the quantity of sugar in the medium was elevated. In the cases in which stearin and glucose were used as co-substrates, in spite of the fact that the quantity of cellular lipid inside the yeast cells varied remarkably (from 0.3 to 2.0 g/l – 4 to 20% wt/wt), de novo fatty acid biosynthesis was observed. This activity increased when the yeast cells assimilated higher sugar quantities. The citric acid produced was mainly derived from the catabolism of sugar. Nevertheless, citric acid yield on sugar consumed and citrate specific production rate, as evaluated by the numerical model, presented substantially higher values in the fermentation in which no fat was used as glucose co-substrate compared with the cultures with stearin used as co-substrate.     

Production of the macrolide antibiotic tylosin in cyclic fed-batch culture

Tylosin-producing Streptomyces fradiae was cultured on a synthetic medium with a high glutamate-glucose ratio. Tylosin batch fermentations with this medium were characterized by a high initial specific production rate of tylosin (q(tylosin), mg/g h) that decreased as the fermentation progressed. Continuous feeding of glutamate, glucose, and methyloleate at a constant feed rate initiated during the period of high q(tylosin) had been shown to produce some increase in tylosin productivity. By using a cyclic feeding strategy, it was possible to increase tylosin productivity further. Tylosin fed-batch fermentations with glutamate and glucose being fed to the culture in cyclic square-wave profiles with methyloleate in excess showed several-fold increase in final q(tylosin) and tylosin titers. By varying cycle amplitudes and period of the substrates, it was found that maximum tylosin productivity occurred when the glutamate cycle amplitude was 600 mg/L and that of glucose was 42.5 mg/L per cycle period of 24 h. With these cycle amplitudes of glutamate and glucose, the tylosin cyclic fed-batch culture also showed high cellular uptake of methyloleate. Decreasing or increasing glucose cycle amplitude at fixed glutamate amplitude lowered tylosin production, and no further stimulation of tylosin synthesis was observed when alpha-ketoglutarate was supplemented to the cyclic substrate feeds. Under optimum cyclic conditions it was possible to maintain linear tylosin accretion and a constant value of q(tylosin) up to 240 h.     

Utilization of by-products derived from bioethanol production process for cost-effective production of lactic acid

The by-products of bioethanol production such as thin stillage (TS) and condensed distillers solubles (CDS) were used as a potential nitrogen source for economical production of lactic acid. The effect of those by-products and their concentrations on lactic acid fermentation were investigated using Lactobacillus paracasei CHB2121. Approximately, 6.7 g/L of yeast extract at a carbon source to nitrogen source ratio of 15 was required to produce 90 g/L of lactic acid in the medium containing 100 g/L of glucose. Batch fermentation of TS medium resulted in 90 g/L of lactic acid after 48 h, and the medium containing 10 % CDS resulted in 95 g/L of lactic acid after 44 h. Therefore, TS and CDS could be considered as potential alternative fermentation medium for the economical production of lactic acid. Furthermore, lactic acid fermentation was performed using only cassava and CDS for commercial production of lactic acid. The volumetric productivity of lactic acid [2.94 g/(L·h)] was 37 % higher than the productivity obtained from the medium with glucose and CDS.